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A kind of hydrogenation catalyst and its application in hydrodeoxygenation

A hydrogenation catalyst and catalyst technology, applied in the field of hydrogenation catalyst and its application in hydrodeoxygenation, can solve the problems of easy deactivation, poor stability, etc.

Active Publication Date: 2017-12-22
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, such catalysts are less stable when applied to hydrodeoxygenation and are easily deactivated

Method used

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  • A kind of hydrogenation catalyst and its application in hydrodeoxygenation
  • A kind of hydrogenation catalyst and its application in hydrodeoxygenation

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0084] Take by weighing 350 grams of CL-A powder and 120 grams of CL-A-600 powder (CL-A-600 powder and the mass ratio of CL-A powder on dry basis are 0.34) in dry basis, and combine them with 3600 grams of deionized water were mixed and stirred to form a slurry; the slurry was transferred to a stainless steel autoclave with a stirring volume of 5 liters and a polytetrafluoroethylene liner, sealed and heated to 160 ° C, and kept at a constant temperature for 4 hours under stirring; Afterwards, after cooling down to room temperature and filtering, the filter cake was dried at 120° C. for 8 hours to obtain the modified product Q-S1. The crystal phase, relative crystallinity and grain size were characterized by X-ray diffraction method, and the results are listed in Table 1.

[0085] Q-S1 is extruded into a clover-shaped strip with a circumscribed circle diameter of 1.6 mm using a extrusion machine (manufacturer: South China University of Technology Science and Technology Industri...

Embodiment 2

[0087] Take by weighing 224 grams of CL-A powder in dry basis, 300 grams of CL-A-600 powder (the ratio of the mass of CL-A-600 powder to the CL-A powder in dry basis is 1.34), and take them Mix and stir with 3600 grams of deionized water to form a slurry; transfer the slurry to a stirred stainless steel autoclave with a polytetrafluoroethylene liner with a volume of 5 liters, seal it and heat it to 160 ° C for 4 hours at a constant temperature; drop to room temperature and After filtration, the filter cake was dried at 120° C. for 8 hours to obtain modified alumina hydrate Q-S2. The crystal phase, relative crystallinity and grain size were characterized by X-ray diffraction method, and the results are listed in Table 1.

[0088] Q-S2 is extruded into a clover-shaped strip with a circumscribed circle diameter of 1.6 millimeters with a extruder (same as embodiment 1). After the wet strip was dried at 120°C for 4 hours, it was kept at 600°C in a muffle furnace for 4 hours under ...

Embodiment 3

[0090] Take by weighing 109 grams of CL-A powder and 464 grams of CL-A-600 powder (CL-A-600 powder and the ratio of the mass of CL-A powder in dry basis to 4.25) in dry basis respectively. Mix and stir with 3600 grams of deionized water to form a slurry; transfer the slurry to a stirred stainless steel autoclave with a polytetrafluoroethylene liner with a volume of 5 liters, seal it and heat it to 160 ° C for 4 hours at a constant temperature; drop to room temperature and After filtration, the filter cake was dried at 120° C. for 8 hours to obtain modified alumina hydrate Q-S3. The crystal phase, relative crystallinity and grain size were characterized by X-ray diffraction method, and the results are listed in Table 1.

[0091] Formed alumina provided by the invention and its preparation:

[0092] Q-S3 is extruded into a clover-shaped bar with a circumscribed circle diameter of 1.6 mm with a bar extruder (same as embodiment 1). After the wet strip was dried at 120°C for 4 ho...

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Abstract

A hydrogenation catalyst containing a carbon-containing shaped refractory oxide support and a molybdenum and / or tungsten metal component selected from group VIB supported on the support and its use in hydrodeoxygenation and nickel and / or cobalt metal components selected from group VIII, the carbon-containing carrier is prepared by a method comprising the following steps: (1) impregnating a solution containing phenolic compounds and / or furan compounds to form a resistant Thermal oxide carrier; (2) the product of step (1) is dried and activated under an inert gas atmosphere; wherein, the amount of each component in the step (1) and the operating conditions in the step (2) make The carbon content in the carrier is 0.1-5% by weight. Compared with existing catalysts, the catalyst provided by the invention has higher hydrodeoxygenation activity and stability.

Description

technical field [0001] The invention relates to a hydrogenation catalyst and its application in hydrodeoxygenation. Background technique [0002] Coal direct conversion oil, Fischer-Tropsch synthetic oil, oil shale, and bio-oil have high oxygen content. High oxygen content directly affects the quality of oil products. Hydrodeoxygenation reaction is required to remove oxygen-containing compounds. [0003] CN 201210237740.8 discloses a non-supported nano-hydrogenation deoxygenation catalyst. The catalyst uses nickel, molybdenum, and tungsten compounds as precursors of active components. The form constitutes the catalyst, and the components of the required precursor are composed by mass percentage: 3%-40% of nickel nitrate, 1%-40% of molybdenum oxide, 1%-70% of tungsten oxide, and 5%-70% of sulfur. The method of constant temperature annealing after high-energy ball milling under the action of protective atmosphere is adopted to prepare nanometer catalyst body particles. It is...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/882C10G45/08
Inventor 李会峰李明丰郑成功褚阳刘锋李大东聂红渠红亮
Owner CHINA PETROLEUM & CHEM CORP